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40                             Enhanced Oil Recovery in Shale and Tight Reservoirs






























              Figure 2.32 Pressure distribution in Core 2 at the end of soaking at Cycle 7.


             Li et al. (2017b) used a simulation model to history match the tests for
          Core 2. Fig. 2.32 shows the pressure distribution in Core 2 at the end of
          soaking period at Cycle 7. It can be seen that the pressure in the central
          part of the core was lower than that near the core surface where the injection
          pressure was reported and plotted in Fig. 2.31. To make the central part
          miscible, the injection pressure near the core surface must be higher than
          the MMP (1620 psi) determined from the slimtube test. This phenomenon
          is less significant in a high-permeability case. Another fact that caused this
          MMP difference is the two methods used. One method is to measure
          MMP from the huff-n-puff tests in which the pressure depletion was fast
          and the pressure was actually lower than the MMP required in the puff
          period. The other is from the slimtube experiments in which the gas injec-
          tion rate in the slimtube experiment was extremely slow to allow the gas to
          fully mix with oil. Therefore, the MMP required for huff-n-puff injection
          should be higher than the MMP estimated from the slimtube tests.
             Similarly, the distributions of CO 2 mole fraction in oil inside the core at
          the end of soaking period in Cycle 7 (Fig. 2.33) shows that when the injec-
          tion pressure was below 1800 psi, the CO 2 fraction in the core center was
          low, indicating the miscibility was not reached. When the pressure was at
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